关键字：MASS-TRANSFER CHARACTERISTICS; IMAGE MEASUREMENT TECHNIQUE; BUBBLE-SIZE DISTRIBUTIONS; CFD SIMULATION; MIXING CHARACTERISTICS; FLUID-DYNAMICS; WASTE-WATER; COLUMN; FLOW; BIOREACTOR

摘要：The multistage internal airlift loop reactor (MIALR) has shown promising application prospects in gas-liquid-solid reaction systems. However, traditional MIALRs have a global circulation with strong interstage liquid-phase exchange. This paper proposes a staggered multistage internal airlift loop reactor (SMIALR) that incorporates special guide elements to create a staggered flow. Both experiments and computational fluid dynamics-population balance model simulations were conducted to investigate the hydrodynamic performances of MIALR and SMIALR. The results demonstrate that SMIALR exhibits a local circulation at each stage. Bubbles have a longer residence time in SMIALR, resulting in a 28.35%-55.54% increase in gas holdup and a 7.27%-13.69% increase in volumetric mass transfer coefficient. The gas-liquid mass transfer coefficient of SMIALR was improved by increasing the gas-liquid interfacial area. Additionally, the radial distribution of solids was found to be more uniform. This study offers insights for optimizing MIALR and provides a theoretical foundation for the design and scale-up of SMIALR.

卷号：36

期号：2

是否译文：否